2005
DOI: 10.2172/861458
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Opportunities for Biorenewables in Oil Refineries

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Cited by 93 publications
(106 citation statements)
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“…This is also claimed by Neste Oil [63], who states better GHG performance for HVO than transesterified lipids from the same feedstock, also supported by Marker et al [64]. Other studies claim similar performance of transesterified lipids and HVO [5].…”
Section: Ranking Of Transesterified Lipids Vs Hvosupporting
confidence: 60%
See 1 more Smart Citation
“…This is also claimed by Neste Oil [63], who states better GHG performance for HVO than transesterified lipids from the same feedstock, also supported by Marker et al [64]. Other studies claim similar performance of transesterified lipids and HVO [5].…”
Section: Ranking Of Transesterified Lipids Vs Hvosupporting
confidence: 60%
“…Around 0.35 million tons crude tall oil diesel could theoretically be produced. Crude tall oil is available at 100-400 USD/ton [64,121,122].…”
Section: Economic Assessment and Resource Availabilitymentioning
confidence: 99%
“…The cost of a small hydrocracker system processing hydrotreated bio-oil has been estimated by UOP (Marker et al 2005). The large-diameter, high-pressure hydrotreater vessels are likely to be manufactured outside of the United States.…”
Section: Pyrolysis Oil Hydrotreating and Hydrocrackingmentioning
confidence: 99%
“…All final processing of the stable oil to fuels occurs in the refinery. VTT and partners (Solantuasta 2006) and UOP (Marker et al 2005, Holmgren et al 2007 are separately pursuing producing bioproducts compatible with existing refinery infrastructure. This will lessen the initial investment; however, direct use of stable oil in a refinery requires complete deoxygenation and a low acid number to prevent corrosion.…”
Section: Co-location With a Refinerymentioning
confidence: 99%
“…The models currently assume that the stated "lipid content" is essentially 100% triglyceride, and thus ignores impurities that may be present such as phospholipids and nitrogen-containing impurities that could require additional cleanup. Additionally, hydrotreating process specifications such as hydrogen demand, pressure, and temperature are based on a compilation of literature studies for hydrotreating vegetable oils (primarily Marker et al 2005), and thus are currently independent of the specific oil characteristics such as degree of saturation. The cost for upgrading is based on a scaling-factor approach for a general hydrotreating plant (in general, the hydrotreating cost is not currently envisioned to present a large economic hurdle).…”
Section: Spent Biomass Utilization (Anaerobic Digestion)mentioning
confidence: 99%